Co/Mo bimetallic addition to electrolytic manganese dioxide for oxygen generation in acid medium

Scientific Reports volume 5, Article number: 15208 (2015) Cite this article

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An efficient electrocatalyst comprising inexpensive and earth-abundant materials for the oxygen evolution reaction (OER) is crucial for the development of water electrolysis. In this work, in-situ addition of cobalt/molybdenum ions to the electrolytic manganese dioxide has been shown to be beneficial for the OER in acid solution as its overpotential performed better (305 mV) than that of the commercial DSA® (341 mV) at 100 mA cm−2. The OER was investigated at ambient temperature in 2 M H2SO4 solution on the modified EMD (MnMoCoO) electrodes. The energy efficiency of the MnMoCoO electrodes improved significantly with the amount of Co in the plating solution. For the electrodeposited catalysts, physico-chemical and electrochemical measurements were conducted including static overpotentials. The better performance of the modified EMD was attributed to an improved charge transfer resistance (Rct; 0.290 Ω cm2), average roughness factor (rf; 429) and decrease in water content in the electrodeposited catalysts. The kinetic parameters obtained on MnMoCoO catalysts were compared and discussed according to the cobalt concentration.

Hydrogen is an abundant, renewable and clean energy source and has been considered as a solution to the problems arising from the current unsustainable fossil fuel economy. Recently, the hydrogen economy is gaining the attention of government bodies and major oil companies1,2,3,4,5,6,7,8. Hydrogen can be generated through various methods including thermochemical, electrochemical and biochemical9. Of all these available methods, water electrolysis (via electrochemical) is suitable for large scale production of hydrogen. Electrolysis of water is a simple way to produce hydrogen with high purity at an economical price when a source of energy to drive the electrolysis is available such as solar or nuclear energy1.

The water electrolysis consists of two electrochemical reactions, termed as hydrogen and oxygen evolution reactions (HER and OER). The equilibrium potential of water electrolysis is 1.23 V at standard conditions but to drive the electrolysis at a practical rate requires higher potentials and this is conventionally measured as overpotential9. The difference between the equilibrium potential and the potential at practical current densities (e.g. 100 mA cm−2) is called polarization or overpotential (η). Metals such as Pt and Ru provide an excellent catalytic surface in lowering the overpotential (η) for the HER10. The most notable catalysts belong to the platinum group metals and are used for the HER, in addition, platinum group oxides11,12,13 are used for the OER. However, platinum group metals are greatly limited by its scarcity and high cost. For instance, technologies such as fuel cells cannot be scaled up because they require expensive catalysts. The most efficient electrocatalyst for the OER are metal oxide electrodes12,13 (RuO2 being the best13, IrO2 also shows good overpotentials11). Oxides present advantages over metal counterparts because they are more stable and cannot be further oxidized. Hence, the desire is to develop an inexpensive noble metal free OER catalyst.

With this as an objective, in our current paper, the use of electrolytic manganese dioxide (EMD, γ type MnO2) with in-situ addition of cobalt/molybdenum ions during electrodeposition (termed modified EMD) has been investigated as a potential catalyst towards the OER. The modified EMD significantly lowers the overpotential of the parent EMD material. Another objective of this work is to investigate the reasons for the decrease in overpotential found with these electrodes while varying the Co content in the bath solution. To the best of our knowledge, modified EMD (MEMD) materials with Co as an additive have not been reported previously. Electrolytic manganese dioxides are a well-researched area in energy storage14 as well as for catalysts to suppress the chlorine evolution reaction15,16,17,18,19 in seawater electrolysis. These studies support the concept of this material for electrochemical applications.

EMD is brittle and adding molybdenum has been found to improve its adherence to the substrate15, 16, 17, 18, 19. Besides molybdenum, a range of other additives in the electrolytic bath have also been investigated15, 16, 17, 18, 19 in the range of 3 to 9 mM. However, the cobalt additive in EMD is little known or not well established and we have used this additive in the range of 3 to 15 mM. The role of cobalt as an additive in MnO2 has different advantages, it lowers the water content which increases the electrical conductivity of the modified EMD, in addition, it makes the material to be energy efficient toward the OER and this is discussed in the current study. The combination of molybdenum and the extent of higher amount of cobalt in the bath, appears to be beneficial for the OER as determined in the present paper. In the design of catalysts for ammonia synthesis, the combination of Co/Mo has been experimentally-theoretically reconciled20 and found to outperform ruthenium (platinum group element). The current novel trend for catalyst design is the combination at the molecular scale of elements (e.g. Mo and Co) which show low and high bond strength with reaction intermediates, to generate intermediate bond strength. This is the region where catalysts operate more efficiently20.

In one of our previous works, we have reported MEMD for the OER in alkaline medium21, where a range of doping elements were investigated. The reported doping elements enhanced the overpotential at a current density of 100 mA cm−2. In the current study, these developed MEMD materials showed a competitive overpotential when used in acid medium, as opposed to our previous work reported for alkaline medium21. It should be noted that the overpotential at a current density of (η10) 10 mA cm−2 has recently received more attention as it is believed to be a representative variable for solar water splitting devices. However, we have used the conventional η1009 and found the results to be promising. The significance of this work lies in the technological improvement in electrode performance when acid medium is the electrolyte.

The electroplating station consisted of the plating solution, a power supply and electrodes; one 70 × 50 × 1 mm 316 stainless steel sheet and one 20 × 10 × 1 mm IrO2/Ti sheet (DSA® acquired from AMAC Corrosion Co.) with one face insulated by ferro-lacquer, as counter and working electrodes, respectively. An internal half-cell vessel connecting the solutions by a Nafion membrane was used. The electrolytic solutions used in the preparation of modified EMDs are tabulated in Table 1. The samples were electrodeposited at i = 10 mA cm−2. The electrodeposited samples were dried at 100 oC in an oven for a period of 1 hour in an air atmosphere and used for all physico-chemical and electrochemical measurements.

The polarization curve was performed on a three electrode set up, remotely controlled by a BioLogic VSP potentiostat. The reference (RE) and counter electrode (CE) were Ag|AgCl in a satd. KCl solution and a platinized platinum sheet with the dimensions of 10 × 10 × 1 mm, respectively. The potential of the Ag|AgCl satd. KCl electrode was taken as 197 mV vs. SHE. Modified EMD based electrodes were made anodic in 2 M H2SO4 solutions in the OER regime. The scan rate was 0.1 mV s−1 and the scan range was set arbitrarily from low to high current density in the range of 1 to 100 mA cm−2. The IRdrop compensation was carried out by the current interruption method. Finally, the geometric area of the coated sample was used in the determination of current densities and all the tests were done at 25 oC. The time dependent current density experiment (under static potential) was done in sequence after cyclic voltammetry with the same set up. A chosen voltage was kept constant for a specific period of time and the current response was monitored.

EIS consisted of 3 consecutive scans over the frequency range from 10 kHz to 0.05 Hz performed sequentially at potentials in the OER regime. The ac sinusoidal voltage applied had amplitude of 5 mV at 25 oC. A fit for purpose argental satd. KCl was used as reference electrode for this test.

The crystallinity of the modified EMD deposits was examined by a Siemens X-ray diffractometer with Philips Co-Kα radiation (1.7902 Å). X-ray photoelectron spectroscopy (XPS) was used to examine the chemical structures in the deposits with a Thermo Multilab 2000. Carbon, C (1 s), was used as the reference spectrum. Finally, the morphology of the deposits was determined by scanning electron microscopy (SEM) equipped with energy dispersive analysis (EDS) for qualitative elemental analysis using two JEOL instruments, models JSM-7000 F and JSM-6000, respectively.

Figure 1 shows the Tafel plot of the modified EMD samples with Co and Mo as additives (MnMoCoO) for the OER in 2 M H2SO4 solution. For all the samples tested, the Tafel lines show one slope close to ~60 mV dec−1 in the low current density region and another slope at around ~115 mV dec−1 in the high current density region. In the supporting information, there is the theory which explains the OER mechanism steps that reconcile the different Tafel slopes found. A change in the magnitude of the Tafel slope indicates different rate determining steps (rds) which can be related to those proposed by different sources10,11. In the OER region the electrodes with varying Co content exhibit different values of overpotential. Table 2 shows the electrochemical parameters of all the tested samples. Among the modified samples studied, the sample with the highest cobalt concentration labelled #5 (i.e. MnMoCoO #5) exhibits the best overpotential (i.e. 305 mV) when compared to that from DSA® at 100 mA cm−2 (i.e. 341 mV). DSA® has been reported to have similar overpotentials (η) and Tafel slopes (b) to those determined by other research groups11,22. Hu et al. reported22 that the oxygen evolution reaction on IrO2 based DSA® electrodes to have Tafel slopes of 59 mV dec−1 and 130 mV dec−1 at low and high overpotentials, respectively. Similar slopes have been determined. At low overpotentials the rate determining step (rds) is that described by Eqs. S-4 and S-5 (in the supporting information). For high overpotentials the rds is described by the Eq. S-1 as it yields a slope of 120 mV dec−1.

Tafel plot of the modified EMD samples in 2 M H2SO4 solution.

The performance characteristics of the MnMoCoO samples have been substantially improved by adding CoSO4 in the plating solution (see Fig. 1 and Table 2). In addition, for the electrode (MnMoCoO #5), current-potential curves were recorded in the forward and backward directions without interruption (Fig. 2a). However, a slight deviation from linearity at high overpotentials is observed. This deviation, could be attributed to ohmic drop. A steady state current potential curve for oxygen evolution has been performed for the best energy efficient sample labeled #5 (Fig. 2b). This potential-static holding has also been undertaken to evaluate the stability of the modified EMD electrode. At a chosen constant overpotential (η = 280 mV) the observed current density over a period of time is found to be constant.

(a) Cyclic voltammetry curve for oxygen evolution (b) Time-dependent current density curve under the constant overpotential η = 280 mV for the MnMoCoO #5 sample (best energy efficient sample) in 2 M H2SO4 solution.

The overpotential of the modified EMD samples in Table 2 for acid electrolyte is found to be superior to those reported from our previous work21 in alkaline electrolyte. A change in the electrolyte, yields different types of adsorbed reaction intermediates (i.e. Eqs. S-1 to S-5 in the supporting information). The bond strength between the catalyst surface and an adsorbed reaction intermediate, changes as a function of the adsorbate chemical structure and this could be the reason of the changes seen in the results for the overpotential found in the OER in different electrolytes. In this respect, other variables such as the exchange current density (io) and charge transfer resistance (Rct) (Rct is explained in the supporting information) do support the results found by Tafel slopes in Fig. 1. These variables (io, Rct) from the MEMD samples show better values to those from DSA® (see Table 2).

The equivalent circuit selected to model the EIS data is the 1CPE model21 (shown in Fig. S-1). Figure 3(a) shows the Nyquist impedance and 3(b) Bode admittance diagrams of the best performed sample (i.e. MnMoCoO #5) to illustrate intermediate data processing results. The curves shown in Fig. 3 are representative for all the MnMoCoO samples studied, which exhibit one capacitive loop that has been interpreted to be related to kinetic control23,24,25. No other capacitive or inductive loops corresponding to mass transfer control or oxide impedance are identified. Variables of importance from the 1CPE model are the CPEdl and Rct, as they provide direct information about the roughness factor and energy efficiency. The charge transfer resistance (Rct) was determined at a current density of 10 mA cm−2 and this variable is close to that of the DSA® sample. The results are tabulated in Table 2. Rct is believed to directly correlate to overpotentials for the OER, as oppose to a high roughness factor, which does not necessarily means that the overpotential (η) will improve. Average roughness factors (rf) have been determined by Eq. S-6 and the corresponding values are tabulated in Table 2. Roughness factors have been determined to be in the same order of magnitude for all the samples, including the DSA®.

(a) Nyquist impedance and (b) Bode admittance diagrams of the MnMoCoO #5 sample at η = 245 mV in 2 M H2SO4 solution. Continuous lines represent the fitted curve by the 1CPE model, experimental data as symbols.

Electrolytic manganese dioxide (EMDs) in general are mainly composed of γ-MnO2 phase and to a small extent by ε-MnO226,27. γ-MnO2 is composed of pyrolusite and ramsdellite structures, they both possess a 110 diffraction line. EMDs have the 021 diffraction peak with the highest intensity followed by the 110 peak27. Figure 4a shows the X-ray diffraction spectra of the modified EMD samples. The control sample and substrate are also included for a comparison to study the degree of changes in the crystallinity. Three diffraction peaks with the reflections (021), (002) and (110) are identified for the standard (control) EMD material (in Fig. 4a) which does not contain the cobalt/molybdenum additives. The 110 peak in the EMD control sample is represented as 110* as the substrate exhibits a peak at the same region, this peak has not been considered for further the analysis.

(a) X-ray diffraction patterns (XRD) of the modified EMD samples. (b) XRD of the MnMoCoO #5 sample (best energy efficient sample) before and after electrochemical measurements indicating the stability of the EMD structure.

For the samples with increasing cobalt additive, labeled #1 to #5 (#5 being the sample with the highest addition of Co, for details refer to Table 1) the XRD spectra show similar peaks to that of the control sample. As the content of cobalt in the EMD solution increases, the (002) peak intensity decreases. However, the (021) peak remains but becomes broad. The observed changes in the crystallinity of the samples could be one of the beneficial factors towards improved overpotential for oxygen generation. To study the chemical stability of the MEMD samples, the sample #5 is selected (best energy efficient sample towards the OER). We have performed XRD analysis before and after electrochemical measurements to determine any changes in the crystalline structure. Figure 4b shows the XRD spectra of the MnMoCoO #5 sample, before and after electrochemical measurement. As observed from the XRD (Fig. 4b) the diffraction patterns are almost identical, indicating no changes in the crystalline structure. This confirms that modified EMD is chemically stable in the acid OER regime.

The γ-MnO2 (EMD) can be described by the chemical formula28,29,30 as:

Where x is the cation vacancy fraction and y is the fraction of Mn3+ ions, replacing Mn4+ in the manganese sub-lattice. EMDs have typical values of x and y as follows: x ≈ 0.06 and y ≈ 0.075. This means that Mn4+ should be the dominant specie in EMDs.

Figure 5 shows the X-ray photoelectron spectroscopy (XPS) of Mn(2p) and O(1s) for the modified EMD samples, including the control sample. Figure 5a shows two peaks in the region where manganese (Mn) species are expected, these peaks correspond to the Mn(2p1/2 and 2p3/2) spin orbit split components. Comparing the XPS (Fig. 5a) results from the modified EMD samples to the standard (control) sample, it can be seen that all the XPS spectra of the samples are similar. This result suggests that the ratio of Mn4+ to Mn3+ in the MEMD is constant despite of increasing the concentration of Co2+ ion in the plating solution.

XPS spectra of the modified EMD samples.

(a) Mn(2p) and (b) O(1s) spectra. A standard (control) EMD sample has been included as number 1.

Figure 5b shows the O(1s) spectra of the samples. Considering the O(1s) peak parameters from Manganite31. The O2−, OH− and H2O peaks are found at 529.6, 530.8 and 531.6 eV, respectively (O2−, OH− and H2O are structural species). Comparing the O(1s) XPS spectra of the samples to the EMD control sample, it can be seen that the EMD control spectra has a shoulder in the region of structural water, other samples do not show this shoulder. In addition, the more Co2+ ion in the plating solution the more intense the O(1s) peak becomes. One could interpret these results as a decrease in water content that would increase the structural oxygen content in the modified EMD coating. The presence of additives (i.e. Co2+ ion) in the plating solution could be suppressing structural water formation during electrodeposition. These results indicate a lower concentration of structural water in the samples than that from the control EMD, which is beneficial for catalytic activity as it increases electrical conductivity and the quantity of active sites.

An additional figure has been included to analyze the chemical stability of the MEMD under the electrochemical test conditions. Figure 6 in combination with Fig. 4b, show the chemical structure of the MnMoCoO #5 sample, before and after cyclic voltammetry. Figures 6 and 4b indicate that the sample #5 is stable for the OER in acid medium.

XPS spectra of the MnMoCoO #5 sample before and after cyclic voltammetry.

Mn(2p) and O(1s) labeled as (a) and (b), respectively.

Figure 7 shows the plan micrograph view of the modified EMD samples (DSA® is shown21) at low and high magnification. These results show that all EMD based samples have a structure similar to that of dry mud. SEM results show an increase of the dry mud polygon size when the Co2+ content in the plating solution is increased when compared to the standard EMD. The SEM micrographs do not show a clear trend about the polygon average area enclosed by cracks as a function of Co2+ content in the plating solution. Bigger polygon sizes would decrease the area of the cracks and surface, this should decrease the roughness factor and hence increase the overpotential. Figure 7g also compares the surface morphology of the MnMoCoO #5 after electrochemical measurements. It is visualized from the micrograph that the morphology is quite similar, indicating that the sample is mechanically stable.

SEM imaging of the modified EMD samples.

(a,c,e) refers to MnMoCoO #3, MnMoCoO #4 and MnMoCoO #5 (low magnification) and (b, d and f) refers to the respective samples at high magnification. Fig. 8(g) refers to MnMoCoO #5 after electrochemical measurement showing a similar morphology to that of Fig. 8(f).

Considering the analysis from XPS and SEM/EDS (Table 3), it is found that the more Co2+ ion content in the plating solution, the lower the water content in the modified EMD electrodeposited samples. It is believed that water in the modified EMD sample does not become an active site and its presence lowers the quantity or energy efficiency of the active sites making the material less electroactive. The electrochemical tests (i.e. Tafel plots and EIS) are closely related to electroactive area which does not have to be the same as the total area (i.e. true area). Water takes space of the surface of the electrode material, which can make the Rct higher or decrease rf depending on whether water becomes or not an active site. It can be seen that Co2+ content in the solution influences the composition of the coating. The higher the Co2+ content the less oxygen is found in the coating and this is in agreement with the results found by XPS, where water content in the modified EMD coating is lowered by Co2+ in solution. This is beneficial as the electrical conductivity of the coating is inversely proportional to water content.

This study suggests that the Co/Mo addition in EMD electrodes played a crucial role. Modified electrolytic manganese dioxide shows a competitive overpotential (305 mV) to that of traditional high-cost DSA® electrodes (341 mV) in acid OER at 100 mA cm−2 and this is supported by electrochemical measurements. The Co2+ ion additive directly influences the structure of MnO2 thus lowering the overpotential for the OER. Among the samples studied in varying the cobalt content, the MnMoCoO #5 sample, is found to be the best in terms of energy efficiency in acid OER than DSA®. The proposed explanation about the lowering of the OER overpotential found in the modified EMD samples can be related to improved combinations of charge transfer resistance and roughness factor. In particular, the charge transfer resistance correlates directly to overpotentials. XPS and EDS show that lowering the water content in the coating increases electrical conductivity, which saves energy.

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We would like to thank AINSE Ltd for providing financial assistance (Award No ALNGRA12020/10366 and AINSE Post Graduate Research Award 10595) to enable work on catalyst surfaces. We would also like to acknowledge the Global R&D Centers Program of NRF (National Research Foundation of Korea), funded by MSIP (Ministry of Science, ICT & Future Planning) at KIGAM (Korean Institute of Geoscience and Mineral Resources) for instrument time.

School of Engineering and Information Technology, Murdoch University, Murdoch, Australia

Dario Delgado, Manickam Minakshi & Justin McGinnity

Mineral Resources Research Division, Korea Institute of Geoscience and Mineral Resources, Daejeon, South Korea

Dong-Jin Kim

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D.D. designed the research, conducted the experiments and wrote the first draft of the manuscript. M.M. significantly contributed in revising the manuscript while J.M and D.K. participated in the discussion of results. M.M and D.K. extended the equipment and characterization facilities.

The authors declare no competing financial interests.

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Delgado, D., Minakshi, M., McGinnity, J. et al. Co/Mo bimetallic addition to electrolytic manganese dioxide for oxygen generation in acid medium. Sci Rep 5, 15208 (2015). https://doi.org/10.1038/srep15208

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Received: 26 May 2015

Accepted: 21 September 2015

Published: 15 October 2015

DOI: https://doi.org/10.1038/srep15208

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